Dishwasher comprising a sorption drying device

ABSTRACT

A dishwasher is provided which has a washing container, an air-guiding channel to generate air flow, and a sorption drying system to dry items to be washed. The sorption drying system has a sorption container with reversibly dehydratable sorption material, wherein the sorption container is connected to the washing container by the air-guiding channel. The reversibly dehydratable sorption material in the sorption container is a granular solid or a granulate having particles with a grain size between 1 mm and 6 mm. The fill height of the particles is at least 5 times the grain size of the particles.

The present invention relates to a dishwasher, in particular a householddishwasher, comprising at least one washing container and at least onesorption drying system for drying items to be washed, the sorptiondrying system having at least one sorption container comprising areversibly dehydratable sorption material, said container beingconnected to the washing container by means of at least one air-guidingchannel for the generation of an air flow.

Dishwashers with a so-called sorption column for drying dishes are knownfor example from DE 103 53 774 A1, DE 103 53 775 A1 or DE 10 2005 004096 A1. In the “drying” subprogram step of the respective dishwashingprogram of the dishwasher for drying dishes, moist air is guided bymeans of a fan out of the washing container of the dishwasher throughthe sorption column and moisture is removed from the air guidedtherethrough by the reversibly dehydratable drying material of saidsorption column through condensation. For regeneration, i.e. desorptionof the sorption column, the reversibly dehydratable drying materialthereof is heated to very high temperatures. Water stored in thismaterial is thereby released as hot water vapor and is guided by an airflow generated by means of the fan into the washing container. A washingliquor and/or dishes located in the washing container, as well as theair located in the washing container can be heated by this means. Asorption column of this type has proven to be highly advantageous forthe energy-saving and quiet drying of the dishes. To avoid localoverheating of the sorption drying material during the desorptionprocess, in DE 10 2005 004 096 A1, for example, a heater is arranged inthe direction of flow of the air, upstream of the air inlet of thesorption column. Despite this “air heating” during desorption, itremains difficult in practice to dry the reversibly dehydratable dryingmaterial consistently adequately and thoroughly.

The underlying object of the invention is to provide a dishwasher, inparticular a household dishwasher, with a further improved sorptiondrying and/or desorption result for the reversibly dehydratable dryingmaterial of the sorption unit of its sorption drying device.

This object is achieved for a dishwasher of the type stated at theoutset in that the sorption material in the sorption container is in theform of a granular solid or granulate comprising a multiplicity ofparticles having a grain size substantially between 1 and 6 mm, inparticular between 2.4 and 4.8 mm, as a fill and that the fill height ofthe particles corresponds to at least 5 times their grain size.

This largely ensures that items to be washed in the washing containercan be dried in a thorough, energy-efficient and reliable manner. Italso makes it possible to accommodate the drying device in thedishwasher in a compact manner.

In particular it is largely ensured that moist air which is guided inthe respective desired drying process via the air guiding channel fromthe washing container into the sorption container and flows through itssorption unit with the sorption material, can be dried with sorption bymeans of the sorption material in a thorough, reliable andenergy-efficient manner. Later, after this drying process, e.g. in atleast one rinsing or cleaning cycle of a later newly-started dishwashingprogram, the sorption material can be regenerated through desorption,i.e. processed again, in a thorough, energy-efficient andmaterial-saving manner in preparation for a subsequent drying process.

Other developments of the invention are described in the subclaims.

The invention and its developments will be described in greater detailbelow with reference to drawings, in which:

FIG. 1 shows schematically a dishwasher comprising a washing containerand a sorption drying system, the components of which are embodiedaccording to the inventive design principle,

FIG. 2 shows schematically in perspective representation the openwashing container of the dishwasher from FIG. 1 with components of thesorption drying system which are partially exposed, i.e. shown uncoveredin the drawing,

FIG. 3 shows in schematic side view the entirety of the sorption dryingsystem from FIGS. 1, 2, the components of which are accommodated partlyexternally on a side wall of the washing container and partly in a basemodule underneath the washing container,

FIG. 4 shows as an individual item schematically in exploded perspectiverepresentation various components of the sorption container of thesorption drying system from FIGS. 1 to 3,

FIG. 5 shows schematically in plan view the sorption container from FIG.4,

FIG. 6 shows in schematic plan view from below, as a component of thesorption container from FIG. 5, a slotted sheet for the flowconditioning of air which flows through sorption material in thesorption container,

FIG. 7 shows in schematic plan view from below, as a further detail ofthe sorption container from FIG. 4, a coiled-tube heater for heatingsorption material in the sorption container for the desorption thereof,

FIG. 8 shows in schematic plan representation, viewed from above, thecoiled-tube heater from FIG. 7 which is arranged above the slotted sheetfrom FIG. 6,

FIG. 9 shows in schematic sectional representation, viewed from theside, the sorption container of FIGS. 4, 5,

FIG. 10 shows in schematic perspective representation the internalstructure of the sorption container of FIGS. 4, 5, 9 in a partiallycutaway state,

FIG. 11 shows in schematic plan representation, viewed from above, theentirety of the components of the sorption drying system of FIGS. 1 to10,

FIGS. 12 to 14 show schematically in various views the outlet element ofthe sorption drying system of FIGS. 1 to 3 as an individual item,

FIG. 15 shows in schematic sectional representation, viewed from theside, the inlet element of the sorption drying system of FIGS. 1 to 3 asan individual item,

FIG. 16 shows in schematic plan representation, viewed from above, thebase module of the dishwasher from FIG. 1 and FIG. 2, and

FIG. 17 shows in schematic representation the thermoelectric heatprotection of the sorption container of FIGS. 4 to 10 of the sorptiondrying system of FIGS. 1 to 3, 11.

Elements having an identical function and mode of operation are in eachcase labeled with the same reference characters in FIGS. 1 to 17.

FIG. 1 shows in schematic representation a dishwasher GS which comprisesas its main components a washing container SPB, a base module BGarranged thereunder and a sorption drying system TS according to theinventive design principle. The sorption drying system TS is preferablyprovided externally, i.e. outside the washing container SPB, partly on aside wall SW and partly in the base module BG. It comprises as its maincomponents at least one air-guiding channel LK, at least one fan unit ora blower LT inserted in said air-guiding channel and at least onesorption container SB. The washing container SB preferably accommodatesone or more mesh baskets GK for receiving and for washing items such asdishes for example. One or more spray devices such as e.g. one or morerotating spray arms SA are provided in the interior of the washingcontainer SPB for spraying the items to be cleaned with a liquid. In theexemplary embodiment here, both a lower spray arm and an upper spray armare suspended to allow them to rotate in the washing container SPB.

To clean items to be washed, dishwashers run through wash programs whichcomprise a plurality of program steps. The respective wash program maycomprise in particular the following individual program steps runningconsecutively over time: A prewash step for removing coarse soiling, acleaning step with the addition of detergent to fluid or water, anintermediate wash step, a rinse step with the application of liquid orwater mixed with wetting agents or rinse aid, and a final drying step inwhich the cleaned items are dried. Depending on the cleaning step orwash cycle of a selected dishwashing program, fresh water and/or usedwater mixed with detergent is applied to the items to be washed in eachcase e.g. for a cleaning cycle, for an intermediate wash cycle and/orfor a final rinse cycle.

The fan unit LT and the sorption container SB are accommodated in theexemplary embodiment here in the base module BG underneath the base BOof the washing container SPB. The air-guiding channel LK runs from anoutlet opening ALA which is provided above the base BO of the washingcontainer SPB in a side wall SW thereof, externally on this side wall SWwith an inlet-end tube portion RA1 down to the fan unit LT in the basemodule BG. The outlet of the fan unit LT is connected by means of aconnecting section VA of the air-guiding channel LK to an inlet openingEO of the sorption container SB in a region thereof close to the base.The outlet opening ALA of the washing container SPB is provided abovethe base BO thereof, preferably in the middle region or in the centralregion of the side wall SW, for sucking air out of the interior of thewashing container SPB. Alternately, it is of course also possible to fixthe outlet opening in the back wall RW (see FIG. 2) of the washingcontainer SPB. Expressed in general terms, it is in particularadvantageous to provide the outlet opening preferably at least above afoam level up to which foam may form in a cleaning cycle, preferably inthe upper half of the washing container SPB in one of the side walls SWand/or back wall thereof. It can optionally also be useful to introducemultiple outlet openings in at least one side wall, top wall and/or theback wall of the washing container SPB and to connect these outletopenings by means of at least one air-guiding channel to one or moreinlet openings in the housing of the sorption container SB before thebeginning or start of the sorption material portion thereof.

The fan unit LT is preferably embodied as an axial fan. It serves toforce moist hot air LU to flow out of the washing container SPB througha sorption unit SE in the sorption container SB. The sorption unit SEcontains reversibly dehydratable sorption material ZEO which can absorband store moisture from the air LU guided through it. The sorptioncontainer SB has an outflow opening AO (see FIGS. 4, 5) on the top sidein the region of its housing close to the cover, said outflow openingbeing connected by means of an outlet element AUS through athrough-insertion opening DG (see FIG. 13) in the base BO of the washingcontainer SPB to the interior thereof. In this way, during a drying stepof a dishwashing program for the drying of cleaned items, moist hot airLU can be sucked by means of the switched-on fan unit LT out of theinterior of the washing container SPB through the outlet opening ALAinto the inlet-end tube portion RA1 of the air-guiding channel LK andtransported via the connecting section VA into the interior of thesorption container SB to be forced to flow through the reversiblydehydratable sorption material ZEO in the sorption unit SE. The sorptionmaterial ZEO in the sorption unit SE extracts water from the moist airflowing through it such that downstream of the sorption unit SE driedair can be blown via the outlet element or exhaust element AUS into theinterior of the washing container SPB. In this way, this sorption dryingsystem TS provides a closed air-circulation system. The spatialarrangement of the various components of this sorption drying system TSwill emerge from the schematic perspective representation of FIG. 2 andthe schematic side view of FIG. 3. In FIG. 3, the course of the base BOis additionally included in the drawing as a dashed and dotted line,which better illustrates the spatial/geometric proportions of the layoutof the sorption drying system TS.

The outlet opening ALA is preferably arranged at a point above the baseBO that enables the collection or suction of as much moist hot air LU aspossible out of the upper half of the washing container SPB into theair-guiding channel LK. This is because, after the cleaning cycle, inparticular final rinse cycle with heated liquid, moist hot air collectspreferably above the base BO, in particular in the upper half, of thewashing container SPB. The outlet opening ALA lies preferably at avertical position above the level of foam which can occur during regularwashing or in the event of a malfunction. In particular, foam can becaused e.g. by detergent in the water during the cleaning cycle. On theother hand, the position of the discharge point or outlet opening ALA ischosen such that for the inlet-end tube portion RA1 of the air-guidingchannel LK a still rising pathway on the side wall SW is freelyavailable. Placing the discharge opening or outlet opening in thecentral area, cover area and/or upper area of the side wall SW and/orback wall RW of the washing container SPB also largely prevents thepossibility of water being injected out of the sump in the base of thewashing container or out of the liquid spraying system thereof throughthe outlet opening ALA of the washing container SPB directly into theair-guiding channel LK and subsequently entering the sorption containerSB, which there could otherwise render inadmissibly moist, partiallydamage or render unusable, or even completely destroy, the sorptionmaterial ZEO thereof.

At least one heating device HZ for desorption and thus regeneration ofthe sorption material ZEO is arranged in the sorption container SBupstream of the sorption unit SE thereof, viewed in the direction offlow. The heating device HZ serves to heat air LU which is driven bymeans of the fan unit LT through the air-guiding channel LK into thesorption container. This forcibly heated air absorbs the storedmoisture, in particular water, from the sorption material ZEO as itflows through the sorption material ZEO. This water which is expelledfrom the sorption material ZEO is transported by the heated air via theoutlet element AUS of the sorption container SB into the interior of thewashing container. This desorption process preferably takes place whenthe heating of liquid for a cleaning cycle or other wash cycle of asubsequent dishwashing program is desired or is being carried out. Inthis case the air heated by the heating device HZ for the desorptionprocess can simultaneously be included for heating the liquid in thewashing container SPB, on its own or to support a conventional waterheater, which is energy-saving.

FIG. 2 shows, with the door TR of the dishwasher GS from FIG. 1 open,the main components of the sorption drying system TS in the side wall SWand the base module BG partially in an exposed state in a perspectiverepresentation. FIG. 3 shows, to accompany this, the totality ofcomponents of the sorption drying system TS, viewed from the side. Theinlet-end tube portion RA1 of the air-guiding channel LK comprises,starting from the vertical position of its inlet opening EI at thelocation of the outlet opening ALA of the washing container SPB, a tubeportion AU that is upwardly rising in relation to the direction ofgravity and thereafter a tube portion AB that is downwardly descendingin relation to the direction of gravity SKR. The upwardly rising tubeportion AU runs somewhat obliquely upward relative to the verticaldirection of gravity SKR and passes into a curved portion KRA, which isconvexly curved and forces, with respect to the inflowing air flow LS1,a reversal of direction of approximately 180° downward into theadjacent, substantially vertically downward descending, tube portion AB.This tube portion ends in the fan unit LT. The first upwardly risingtube portion AU, the curved portion KRA and the downstream, second,downward descending tube portion AB form a flat channel having asubstantially flatly rectangular cross-sectional geometric shape.

One or more flow-guiding ribs or drainage ribs AR are provided in theinterior of the curved portion KRA, said ribs following the curvedcourse thereof. In the exemplary embodiment, several arc-shaped drainageribs AR are arranged substantially nested concentrically into oneanother and set at a transverse distance from one another in theinterior of the curved portion KRA. They also extend in the exemplaryembodiment here into the rising tube portion AU and into the descendingtube portion AB over part of their length. These drainage ribs AR arearranged in vertical positions above the outlet ALA of the washingcontainer SPB and of the inlet EI of the inlet-end tube portion RA1 ofthe air-guiding channel LK. These drainage ribs AR serve to absorbdroplets of liquid and/or condensation from the air flow LS1 sucked outof the washing container SPB. In the region of the section of theupwardly rising tube portion AU, the droplets of liquid collected on theflow-guiding ribs AR can drip in the direction of the outlet ALA. In theregion of the downwardly descending tube portion AB, the droplets ofliquid can drip from the flow-guiding ribs AR in the direction of atleast one return rib RR. The return rib RR is provided at a point in theinterior of the descending tube portion AB which lies higher than theoutlet opening ALA of the washing container SPB and/or which lies higherthan the inlet opening EI of the air-guiding channel LK. The return ribRR in the interior of the descending tube portion AB forms a drainageincline and aligns with a cross-connecting line RF in the direction ofthe outlet ALA of the washing container SPB. The cross-connecting lineRF bridges the intermediate space between the arm of the upwardly risingtube portion AU and the arm of the downwardly descending tube portionAB. The cross-connecting line RF consequently connects the interior ofthe upwardly rising tube portion AU and the interior of the downwardlydescending tube portion AB to one another. The gradient of the returnrib RR and of the adjacent, aligned cross-connecting line RF is chosenin such a way as to ensure a return of condensation and/or other dropsof liquid which drip down from the drainage ribs AR in the region of thedescending tube portion AB into the outlet opening ALA of the washingcontainer SPB.

The drainage ribs AR are preferably fitted on the inner wall of theair-guiding channel LK facing away from the washing container side wallSW because this exterior inner wall of the air-guiding channel is coolerthan the inner wall of the air-guiding channel facing toward the washingcontainer SPB. On this cooler inner wall condensation precipitates moreintensely than on the inner wall of the air-guiding channel LK facingtoward the side wall SW. Thus, it may suffice for the drainage ribs ARto be embodied as web elements which project from the outward lyinginner wall of the air-guiding channel LK only over a partial width ofthe total cross-sectional width of the air-guiding channel embodied as aflat channel in the direction of the inward-lying inner wall of theair-guiding channel facing the side wall SW, such that a lateralcross-sectional gap relative to the air through-flow remains. It may,however, optionally also be useful to embody the drainage ribs ARbetween the outward lying inner wall and the inward lying inner wall ofthe air-guiding channel LK continuously. In this way, particularly inthe curved portion KRA, a more targeted guidance of air can be achieved.Disruptive air turbulence is largely avoided. A desired volume of aircan in this way be conveyed through the air-guiding channel LK embodiedas a flat channel.

The return rib RR is preferably fitted as a web element on the inside ofthe outward-lying inner wall of the air-guiding channel LK, said webelement projecting over a partial width or partial extent of the totalextent of the flat-design air-guiding channel LK in the direction of theinward-lying inner wall thereof. This ensures that an adequate passagecross-section remains free in the region of the return rib RR for theair flow LS1 to flow through. Alternatively, it can of course also beuseful to embody the return rib RR as a continuous element between theoutside inner wall and the inward-lying inner wall of the air-guidingchannel LK and to provide in particular centrally located passageopenings for the passage of air.

The drainage ribs AR and the return rib RR serve in particular toseparate water droplets, detergent droplets, rinse aid droplets and/orother aerosols which are found in the inflowing air LS1 and to returnthem through the outlet opening ALA into the washing container SPB. Thisis particularly advantageous in a desorption process when a cleaningstep is taking place simultaneously. During this cleaning step, arelatively large amount of steam or mist may be located in the washingcontainer SPB, in particular due to the spraying of washing solution bymeans of the spray arms SA. Such steam or mist may contain both waterand detergent, rinse aid and/or optionally other cleaning substancesfinely distributed. For these dispersed liquid particles carried alongin the air flow LS1, the drainage ribs AR form a separating device.Instead of drainage ribs AR, other separating means can alternately alsoadvantageously be provided, in particular structures having amultiplicity of edges such as e.g. wire meshes.

In particular, the obliquely upwardly or substantially vertically risingtube portion AU ensures that liquid droplets or even spray jets whichare sprayed out by a spraying device SA such as, for example, a sprayarm, during the cleaning cycle or other wash cycle, are largelyprevented from being able to reach the sorption material of the sorptioncontainer directly via the sucked-in air flow LS1. Without thisretention or this separation of liquid droplets, in particular mistdroplets and steam droplets, the sorption material ZEO could be renderedinadmissibly moist and unusable for a sorption process in the dryingstep. In particular, premature saturation could occur due to theinfiltration of liquid droplets such as e.g. mist droplets or steamdroplets. The inlet-end rising branch AU of the through-channel and/orthe one or more separating and capturing elements in the upper bendregion and apical region of the curved portion KRA between the risingbranch AU and the descending branch AB of the through-channel moreoveralso largely prevent detergent droplets, rinse-aid droplets and/or otheraerosol droplets from being able to pass further down beyond thisbarrier to the fan LT and from there into the sorption container SB. Ofcourse, it is also possible to provide in place of the combination ofrising tube portion AU and descending tube portion AB and in place ofthe one or more separating elements a differently-embodied barrierarrangement with the same function.

To sum up, the dishwasher GS in the exemplary embodiment here comprisesa drying device for drying items to be washed through sorption by meansof reversibly dehydratable sorption material ZEO which is stored in asorption container SB. Said sorption container is connected via at leastone air-guiding channel LK to the washing container SPB for generatingan air flow LS1. The air-guiding channel has along its inlet-end tubeportion RA1 a substantially flatly rectangular cross-sectional geometricshape. Viewed in the direction of flow, after its inlet-end tube portionRA1, the air-guiding channel passes into a substantially cylindricaltube portion VA. It is preferably manufactured from at least one plasticmaterial. It is arranged in particular in the intermediate space betweena side wall SW and/or back wall RW of the washing container and an outerhousing wall of the dishwasher. The air-guiding channel LK comprises atleast one upwardly rising tube portion AU. It extends upward startingfrom the discharge opening ALA of the washing container SPB. It alsocomprises after the rising tube portion AU, viewed in the direction offlow, at least one downwardly descending tube portion AB. At least onecurved portion KRA is provided between the rising tube portion AU andthe descending tube portion AB. The curved portion KRA has in particulara greater cross-sectional area than the rising tube portion AU and/orthe descending tube portion AB. One or more flow-guiding ribs AR forequalizing the air flow LS1 are provided in the interior of the curvedportion KRA. At least one of the flow-guiding ribs AR optionally extendsbeyond the curved portion KRA into the rising tube portion AU and/ordescending tube portion AB. The one or more flow-guiding ribs AR areprovided in positions above the vertical position of the outlet ALA ofthe washing container SPB. The respective flow-guiding rib AR extendsfrom the channel wall facing the washing-container housing to theopposing channel wall of the air-guiding channel LK facing away from thewashing-container housing preferably substantially continuously. Atleast one return rib RR is provided in the interior of the descendingtube portion AB on the channel wall facing the washing-container housingand/or channel wall of the air-guiding channel LK facing away from thewashing-container housing at a point which lies higher than the inletopening EI of the air-guiding channel LK. The return rib RR is connectedto the inlet opening EI of the air-guiding channel LK via across-connecting line RF in the intermediate space between the risingtube portion AU and the descending tube portion AB for returningcondensate. It exhibits a gradient toward the inlet opening EI. Thereturn rib extends from the channel wall facing the washing-containerhousing to the opposing channel wall of the air-guiding channel LKfacing away from the washing-container housing preferably only over apartial cross-sectional width.

In FIG. 3, the descending branch AB of the air-guiding channel LK isintroduced substantially vertically into the fan unit LT. The air flowLS1 which is sucked in is blown by the fan unit LT at the output end viaa tubular connecting section VA into an inlet connecting piece ES of thesorption container SB coupled thereto into the region in the vicinity ofthe base thereof. The air flow LS1 flows into the lower region of thesorption container SB with an inflow direction ESR and switches to adifferent flow direction DSR with which it flows through the interior ofthe sorption container SB. This through-flow direction DSR runs frombottom to top through the sorption container SB. In particular, theinlet connecting piece ES steers the incoming air flow LS1 into thesorption container SB in such a way that said air flow is diverted fromits inflow direction ESR in particular by approximately 90 degrees intothe through-flow direction DSR through the sorption container SB.

In accordance with FIG. 3, the sorption container SB is arrangedunderneath the base BO in a base module BG of the washing container SPBin a largely freely-suspended manner such that for heat protection ithas a predefined minimum gap distance LS in relation to neighboringcomponents and/or parts of the base module BG (see also FIG. 10). Forthe sorption container SB attached in a freely-suspended manner underthe base BO of the washing container, here the cover element of the basemodule BG, at least one transport securing element TRS is provided belowsaid sorption container at a predefined clearance distance FRA such thatthe sorption container SB is supported from below in case the sorptioncontainer SB moves down from its freely-suspended position duringtransport. The sorption container SB comprises at least in the region ofits sorption unit SE, in addition to its inner housing IG, at least oneouter housing AG such that its total housing is embodied in adouble-walled manner. Consequently, an air gap clearance LS is presentbetween the inner housing IG and the outer housing AG as a thermalinsulation layer. The fact that the sorption container SB is embodied atleast around the region in which its sorption unit SE is mountedpartially or wholly in at least a double-walled manner provides, inaddition to or independently of the freely-suspended mounting oraccommodation of the sorption container SB, further overheatingprotection in order to adequately protect any neighboring parts orcomponents of the base module BG against inadmissibly high overheatingor combustion.

Expressed in general terms, the housing of the sorption container SB hasa geometric shape such that circumferentially an adequate gap distanceexists from the other parts and components of the base module BG as heatprotection. For example, the sorption container SB has for this purposeon its housing wall SW2 facing the back wall RW of the base module BG anarched shape AF which corresponds to the geometric shape of the backwall RW facing it.

The sorption container SB is mounted on the underside of the base BO, inparticular in the region of a through-opening DG (see FIG. 3, 13) of thebase BO of the washing container SPB. This is illustrated in particularin the schematic side view of FIG. 3. There, the base BO of the washingcontainer SPB has, starting from its outer edges ARA a gradient runningtoward a liquid collecting area FSB. The sorption container SB ismounted on the base BO of the washing container SPB in such a way thatits cover part DEL runs substantially parallel to the underside of thebase BO and at a predefined gap distance LSP therefrom. For positioningthe sorption container SB in a freely-suspended manner, a couplingconnection is provided between at least one coupling component on theunderside of the base, in particular a socket SO, of the sorptioncontainer SB and a component on the top side of the base, in particularthe outlet element AUS, of the sorption container SB in the region of athrough-opening DG in the base BO of the washing container SPB. As acoupling connection, a clamping connection, in particular, is provided.The clamping connection may be formed by a detachable connection, inparticular screw connection, with or without bayonet catch BJ (see FIG.13) between the component of the sorption container SB on the undersideof the base and the component of the sorption container SB on the topside of the base. An edge zone RZ (see FIG. 13) around the onethrough-opening DG of the base BO is clamped between an outlet componenton the underside of the base such as e.g. SO of the sorption containerSB, and the outlet element or spray protection component AUS arrangedabove the base BO. In FIG. 13, the base BO and subpart on the undersideof the base are, for the sake of simplifying the drawing, indicatedmerely by dot-dash lines. The outlet component on the underside of thebase and/or the spray protection component AUS on the top side of thebase projects with its end-face end portion through the through-openingDG of the base BO. The outlet part on the underside of the basecomprises a socket SO around the discharge opening AO of the cover partDEL of the sorption container SB. The spray protection component AUS onthe top side of the base comprises an outflow connecting piece AKT and aspray protection hood SH. At least one sealing element DI1 is providedbetween the component AUS on the top side of the base and the componentSO on the underside of the base.

In summary, the sorption container SB is thus arranged beneath the baseBO of the washing container SPB in a largely freely-suspended mannersuch that for heat protection it has a predefined minimum gap distanceLSP in relation to neighboring components and parts of the base moduleBG. Below the sorption container SPB a transport securing element TRS isadditionally fixedly attached at a predefined clearance distance FRA tothe base of the base module. This transport securing element TRS servesto brace, if necessary from below, the sorption container SB mounted ina freely-suspended manner below the base BO of the washing containerSPB, if said sorption container oscillates downward together with thebase BO, for example during transportation, due to vibrations. Thistransport securing element TRS may, in particular, be formed by a metalbracket bent downward in a U-shaped manner which is fixedly mounted onthe base of the base module. The sorption container SB has on the top ofits cover part DEL the outflow opening AO. An upwardly projecting socketSO is fitted around the outer rim of this outflow opening AO. Acylindrical socket connection element STE is fitted in the approximatelycircular opening of this socket SO (see FIGS. 4, 5, 9, 13), said elementprojecting upwardly and serving as a counterpart to the outflowconnecting piece or exhaust chimney connecting piece AKT to be fastenedthereto. It preferably has an external thread with integrated bayonetcatch BJ, which interacts appropriately with the internal thread of theexhaust chimney connecting piece AKT. The socket SO has on its topseating edge running concentrically around the socket connecting pieceSTE the sealing ring DI1. This is illustrated in FIGS. 3, 4, 9, 13. Thesorption container SB rests firmly pressed with this sealing ring DI1against the underside of the base BO. It is held by the height of thesocket SO at a distance or spacing LSP from the underside of the baseBO. The exhaust chimney connecting piece AKT is inserted down throughthe through-opening DG of the base BO from the top of the base BO andscrewed to the counterpart socket connecting piece STE and secured fromopening by the bayonet catch BJ. The exhaust chimney connecting pieceAKT abuts firmly, encircling the outer edge zone RZ of the base BOaround the through-opening DG with its annular outer edge APR. This isbecause the outer edge zone RZ of the base BO around the through-openingDG is clamped in a liquid-tight manner between an encircling lowerseating edge APR of the exhaust chimney connecting piece AKT and theupper seating edge of the socket AO by means of the sealing ring DI1arranged there. Since the sealing ring DI1 presses on the base BO fromthe underside, it is protected against any impairments or damage bydetergents in the washing solution from ageing. A liquid-tightthrough-connection between the exhaust chimney connecting piece AKT andthe socket SO is formed in this way. This simultaneously functionsadvantageously as a suspension device for the sorption container SB.

The fact that the socket SO projects by a socket height LSP above theremaining surface of the cover part DEL ensures that a gap clearance ispresent between the cover part DEL and the underside of the base BO. Thebase BO of the washing container SPB in the exemplary embodiment herefrom FIG. 3 runs, starting from its encircling edge zone with the sidewalls SW and the back wall RW, with a gradient in an obliquely inclinedmanner toward a preferably central liquid-collecting area FSB. The pumpsump PSU of a circulating pump UWP may be located therebelow (see FIG.16). In FIG. 3, this base BO running from the outside inward at anincline toward the lower lying collecting area FSB is drawn in dashedand dotted lines. The arrangement of the pump sump PSU with thecirculating pump UWP sitting therein underneath the lower lyingcollecting area FSB can be seen from the plan-view image of the basemodule from FIG. 16. The sorption container SB is preferably mounted onthe base BO of the washing container SPB such that its cover part DELruns substantially parallel to the underside of the base BO and at apredefined gap distance LSP therefrom. To this end, the socket SO isplaced on the socket connecting piece STE sitting therein obliquely atan appropriate angle of inclination relative to the surface normal ofthe cover part DEL.

According to FIGS. 4 to 10, the sorption container SB comprises apot-type housing part GT which is closed by means of a cover part DEL.There is provided in the pot-type housing part GT at least the sorptionunit SE comprising reversibly dehydratable sorption material ZEO. Thesorption unit SE is accommodated in the pot-type housing part GT in sucha way that an air flow LS2 can flow through its sorption material ZEOsubstantially in or against the direction of gravity, said air flow LS2being generated through diversion of the air flow LS1 brought via theair-guiding channel LK. The sorption unit SE comprises at least onelower sieve element or grid element US and at least one upper sieveelement or grid element OS at a predefinable vertical distance H fromone another (see in particular FIG. 9). The spatial volume between thetwo sieve elements or grid elements US, OS is to a large extentcompletely filled with the sorption material ZEO. At least one heatingdevice HZ is provided in the pot-type housing part GT. In the pot-typehousing part GT, said heating device is, viewed in the through-flowdirection DSR of the sorption container SB, provided in particularupstream of the sorption unit SE comprising the reversibly dehydratablesorption material ZEO. The heating device HZ is provided in a lowercavity UH of the pot-type housing part GT for collecting inflowing airLS1 from the air-guiding channel LK. The inlet opening EO for theair-guiding channel LK is provided in the pot-type housing part GT. Thedischarge opening AO for the outlet element AUS is provided in the coverpart DEL. A heat-resistant material, in particular metal sheet,preferably stainless steel or a stainless steel alloy, is preferablyused for the cover part DEL and the pot-type housing part GT. The coverpart DEL closes off the pot-type housing part GT to a large extenthermetically. The circumferential outer edge of the cover part DEL isconnected to the upper edge of the pot-type housing part GT only by amechanical connection, in particular by a deforming connection, ajoining connection, a latching connection, a clamping connection, inparticular by a beaded connection or a clinched connection. The pot-typehousing part GT comprises one or more side walls SW1, SW2 (see FIG. 5)which run substantially vertically. It has an external contour whichcorresponds substantially to the internal contour of an installationarea EBR provided for it, in particular in a base module BG (see FIG.16). The two adjacent side walls SW1, SW2 have external surfaces whichrun substantially at right angles to one another. At least one side wallsuch as e.g. SW2, has at least one shape such as e.g. AF which isembodied in a substantially complementary manner to match a shape on theback wall and/or side wall of the base module BG, which is providedunder the base BO of the washing container SPB. The sorption containerSB is provided in a rear corner area EBR between the back wall RW and anadjacent side wall SW of the dishwasher GS, in particular the basemodule BG thereof.

The pot-type housing part GT comprises at least one through-opening DUFfor at least one electrical contact element AP1, AP2 (see FIG. 4). Adrip-protection sheet TSB is mounted in a roofing area above thethrough-opening DUF at least over the extension thereof. Thedrip-protection sheet TSB has a drainage incline.

FIG. 4 shows in a schematic and perspective exploded view the variouscomponents of the sorption container SB in a disassembled state. Thecomponents of the sorption container SB are arranged in multiplepositional planes above one another. This structural design, layeredfrom bottom to top, of the sorption container SB is illustrated inparticular in the sectional view of FIG. 9 and in the sliced perspectiverepresentation of FIG. 10. The sorption container SB comprises the lowercavity UH close to the base for collecting inflowing air from the inletconnecting piece ES. Above this lower cavity UH sits a slotted sheet SKwhich serves as a flow-conditioning means for a coiled-tube heater HZarranged thereabove. The slotted sheet SK sits on a circumferentialsupporting edge around the interior of the sorption container SB. Thissupporting edge has a predefined vertical distance relative to the innerbase of the sorption container SB for forming the lower cavity UH. Theslotted sheet SK preferably has one or more clamping parts in order toclamp it laterally or on the side to a partial surface, to at least oneinner wall of the sorption container SB. A reliable securing in positionof the slotted sheet SK can be provided by this means. In accordancewith the view of the slotted sheet from below of FIG. 6, this slottedsheet has slots SL which substantially follow the course of the coil ofthe coiled-tube heater arranged over the slotted sheet. The slots orpassages SL of the slotted sheet SK are embodied larger, in particularwider or broader, at those locations at which the air flow LS1 enteringthe sorption container SB has a lower velocity in the through-flowdirection DSR through the sorption container SB than at those locationsat which the air flow LS1 entering the sorption container has a greatervelocity in the through-flow direction DSR through the sorptioncontainer SB. This achieves to a large extent an equalization of thelocal flow cross-sectional profile of the air flow LS2, which flowsthrough the sorption container SB from bottom to top in a through-flowdirection DSR. Within the scope of the invention, equalization of thelocal flow cross-sectional profile of the air flow is understood inparticular to mean that substantially the same volume of air passesthrough with approximately the same flow velocity substantially at everyentry point of a through-flow surface.

The coiled-tube heater RZ is arranged, viewed in the direction offlow-through DSR, with a predefined vertical clearance behind theslotted sheet SK. To achieve this, it can be held by means of amultiplicity of sheet parts BT which are embodied in a web-like mannerat a vertical distance above the passages SL. These sheet parts BT (seeFIG. 6) support preferably alternately from below and from above the runof the coiled-tube heater. This makes it possible firstly for thecoiled-tube heater HZ to be reliably secured in position above theslotted sheet SK. Secondly, warping of the slotted sheet SK which canoccur under the heat generated by the coiled-tube heater HZ is largelyavoided. Viewed in the through-flow direction DSR, the coiled-tubeheater HZ is followed by a free intermediate space ZR (see FIG. 9) untilthe rising, substantially from bottom to top, air flow LS2 enters theinlet cross-sectional area SDF of the sorption unit SE. This sorptionunit SE comprises on the inlet side a lower sieve element or gridelement US. An outlet-side upper sieve element or grid element OS isprovided at a vertical distance H from this sieve element or gridelement US. For the two sieve elements US, OS, supporting edges areprovided in portions of or all around the inner walls of the sorptioncontainer in order to position and to hold the sieve elements US, OS intheir assigned vertical position. The two sieve elements US, OS arepreferably arranged parallel to one another at this predefined verticaldistance H. Between the lower sieve element US and the upper sieveelement OS, the sorption material ZEO is filled such that the volumebetween the two sieve elements US, OS is largely completely filled. Whenthe sorption container SB is in the installed state, the inlet-end sieveelement US and the outlet-end sieve element OS are arranged, relative tothe vertically running central axis of the sorption container SB andrelative to the through-flow direction DSR thereof, in substantiallyhorizontal positional planes above one another at the predefinedvertical distance H from one another. In other words, the sorption unitSE is therefore formed in the exemplary embodiment here by a fillingvolume of sorption material ZEO between a lower sieve element US and anupper sieve element OS. Viewed in the through-flow direction DSR, theupper cavity OH for collecting outflowing air is provided above thesorption unit SE. This outflowing air LS2 is guided by the outlet AO ofthe socket connecting piece STE into the exhaust chimney connectingpiece ATK, from where it is blown out into the interior of the washingcontainer SPB.

Flow-conditioning or flow-influencing of the flow LS2 rising from bottomto top in the through-flow direction DSR is performed by the slottedsheet SK such that substantially the same air volume flow flows aroundthe coiled-tube heater substantially at each point of its longitudinalextent. The combination of slotted sheet and coiled-tube heater HZarranged thereabove to a large extent ensures that the air flow LS2 canbe heated largely uniformly during the desorption process upstream ofthe intake area of the lower sieve US. The slotted sheet therebyprovides for a largely uniform local distribution of the heated airvolume flow viewed over the intake cross-sectional area SDF of thesorption unit SE.

In addition to or independently of the slotted sheet SK, it canoptionally also be useful to provide a heating device outside thesorption container SB in the connecting section between the fan unit LTand the inlet opening of the sorption container SB. Because the passagecross-sectional area of this tubular connecting section VA is less thanthe average cross-sectional area of the sorption container SB for an airflow, the air flow LS1 may, before it enters the sorption container SB,already be heated largely uniformly for the desorption process inadvance. The slotted sheet SK can then optionally be omitted completely.

Particularly if the heating of the air is carried out by means of aheating device in the sorption container SB, it can optionally also beuseful to provide, viewed in the through-flow direction DSR of thesorption container SB, both upstream and downstream of the heatingdevice HZ at least one flow-conditioning element in each case such thatapproximately the same air volume flow can flow at each point throughthe amount by volume of sorption material ZEO behind the inletcross-sectional area SDF of the lower sieve element US. In this way, inparticular also during the sorption process during which the heatingdevice HZ is deactivated, i.e. is switched off, it is largely achievedthat all the sorption material is to a large extent completely involvedin the dehumidification of the through-flowing air LS1. In an analogousmanner, in the desorption process in which the through-flowing air LS2is heated up by the heating device HZ, stored water is caused tore-emerge from all the sorption material in the intermediate spacebetween the two sieve elements US, OS such that at all points insidethis spatial volume the sorption material ZEO can be made available,substantially fully dried and thus regenerated, for a subsequent dryingprocess.

The through-flow cross-sectional area SDF of the sorption unit SE in theinterior of the sorption container SB is embodied in the exemplaryembodiment here to be greater than the average cross-sectional area ofthe inlet connecting piece ES on the end of the air-guiding channel LKor of the tubular connecting section VA. The through-flowcross-sectional area SDF of the sorption material is preferably embodiedto be between 2 and 40 times, in particular between 4 and 30 times,preferably between 5 and 25 times greater than the averagecross-sectional area of the inlet connecting piece ES of the air-guidingchannel LK with which said connecting piece opens into the intakeopening EO of the sorption container SB.

In summary, the sorption material ZEO fills a fill volume between thelower sieve element US and the upper sieve element OS so that it has theflow intake cross-sectional area SDF and a flow dischargecross-sectional area SAF substantially perpendicular to the through-flowdirection DSR which runs substantially in a vertical direction. Thelower sieve element US, the upper sieve element OS and the sorptionmaterial ZEO embedded therebetween each have penetration areas which arecongruent in relation to one another for the through-flowing air LS2.This largely ensures that at each point in the volume of the sorptionunit SE, the sorption material thereof can be subjected to approximatelythe same volume flow. During desorption, points of overheating and thusany overloading or other damage to the sorption material ZEO are in thisway largely prevented. During sorption, uniform absorption of moisturefrom the moist air to be dried and thus optimum use of the sorptionmaterial ZEO provided in the sorption unit SE is consequently enabled.

Summing up in general terms, it can therefore be useful to provide oneor more flow-conditioning elements SK in the sorption container SBand/or in an inlet-end tube portion VA, ES of the air-guiding channelLK, in particular downstream of at least one fan unit LT inserted intothe air-guiding channel LK, with one or more air passages SL such thatequalization of the local flow cross-sectional profile of the air flowLS2 is effected when flowing through the sorption container SB in thethrough-flow direction DSR thereof, said through-flow direction beingoriented from bottom to top. Viewed in the through-flow direction DSR ofthe sorption container SB, at least one flow-conditioning element SK isprovided in the lower cavity UH thereof at a vertical distance upstreamof the heating device HZ. In the exemplary embodiment here, a slottedsheet or perforated sheet is provided as the flow-conditioning element.The slots SL in the slotted sheet SK substantially trace the course ofthe winding of a coiled-tube heater HZ which is positioned as a heatingdevice at a clearance distance above the slots SL in the slotted sheet.The slotted sheet is arranged substantially parallel to and at aclearance distance from the air intake cross-sectional area SDF of thesorption unit SE of the sorption container SB. Air passages, inparticular slots SL, in the flow-conditioning element SK are embodied soas to be larger at those locations at which the air flow LS1 enteringthe sorption container SB in the through-flow direction DSR of thesorption container SB has a lower velocity than at those locations atwhich the air flow LS1 entering the sorption container SB in thethrough-flow direction DSR of the sorption container SB has a greatervelocity.

In summary, the sorption drying system TS exhibits the followingspecific flow conditions in the region of the sorption container SB. Theair-guiding channel LK is coupled to the sorption container SB such thatthe entering air flow LS1 opens into the sorption container SB with adirection of inflow ESR and passes into a through-flow direction DSRwhich is different therefrom, with which it flows through the interiorof the sorption container SB. The outflow direction of the air flow LS2exiting the sorption container SB preferably corresponds substantiallyto the through-flow direction DSR. The tube portion RA1 of theair-guiding channel LK opens into the sorption container SB such thatits inflow direction ESR is diverted into the through-flow direction DSRof the sorption container SB, in particular by between 45° and 135°,preferably by approximately 90°. Viewed in the direction of flow,upstream of the sorption container SB at least one fan unit LT isinserted into the inlet-end tube portion RA1 of the air-guiding channelLK for generating a forced air flow LS1 in the direction of at least oneintake opening EO of the sorption container SB. The fan unit LT isarranged in the base module BG underneath the washing container SPB. Thethrough-flow cross-sectional area SDF for the sorption material ZEO inthe interior of the sorption container SB is embodied so as to begreater than the passage cross-sectional area of the inlet connectingpiece ES of the air-guiding channel LK with which said air-guidingchannel opens into the inlet opening EO of the sorption container SB.The through-flow cross-sectional area SDF of the sorption container SBis preferably embodied so as to be between 2 and 40 times, in particularbetween 4 and 30 times, preferably between 5 and 25 times, greater thanthe passage cross-sectional area of the inlet connecting piece ES on theend of the air-guiding channel LK with which said air-guiding channelopens into the intake opening EO of the sorption container SB. At leastone sorption unit SE comprising sorption material ZEO is accommodated inthe sorption container such that air LS1 can flow through the sorptionmaterial ZEO substantially in or against the direction of gravity, saidair being guided out of the washing container SPB into the sorptioncontainer SB via the air-guiding channel LK. The sorption unit SE of thesorption container SB comprises at least one lower sieve element or gridelement US and at least one upper sieve element or grid element OS at apredefinable vertical distance H from one another, the spatial volumebetween the two sieve elements or grid elements US, OS being largelycompletely filled with the sorption material ZEO. The intakecross-sectional area SDF and the discharge cross-sectional area SAF ofthe sorption unit SE of the sorption container SB are chosen so as to bein particular substantially equal in size. The intake cross-sectionalarea SDF and the discharge cross-sectional area SAF of the sorption unitSE of the sorption container SB are furthermore usefully arrangedsubstantially congruently in relation to one another. The sorptioncontainer comprises, viewed in its through-flow direction DSR, at leastone layering comprising a lower cavity UH and a sorption unit SEarranged thereabove, arranged downstream in the through-flow directionDSR. It has in its lower cavity UH at least one heating device HZ. Thesorption container SB comprises above its sorption unit SE at least oneupper cavity OH for collecting outflowing air LS2. The sorption materialZEO fills a fill volume in the sorption unit SE of the sorptioncontainer SB such that a flow intake cross-sectional area SDF arrangedsubstantially perpendicular to the through-flow direction DSR and a flowdischarge cross-sectional area SAF arranged largely parallel thereto isformed. The sorption container has in its upper cover part DEL at leastone outflow opening AO which is connected with the aid of at least oneoutflow component AKT via a through-opening DG in the base BO of thewashing container SPB to the interior thereof.

The sorption material ZEO is advantageously embedded in the sorptioncontainer SB in the shape of the sorption unit SE such that asubstantially equal air volume flow value can be applied tosubstantially each entry point to the through-passage cross-sectionalarea SDF of the sorption unit SE. An aluminum- and/orsilicon-oxide-containing, reversibly dehydratable, material, silica geland/or zeolite, in particular type A, X, Y zeolite, is preferablyprovided, either singly or in any combination, as the sorption materialZEO. The sorption material is provided in the sorption container SBusefully in the form of a granular solid or granulate comprising amultiplicity of particles having a grain size substantially between 1and 6 mm, in particular between 2.4 And 4.8 mm, as a fill, the fillheight H of the particles corresponding to at least 5 times their grainsize. The sorption material ZEO present as a granular solid or granulateis usefully present in the sorption container with a fill height H inthe direction of gravity which corresponds to substantially 5 to 40times, in particular 10 to 15 times the particle size of the granularsolid or granulate. The fill height of the sorption material ZEO ispreferably chosen so as to be substantially between 1.5 and 25 cm, inparticular between 2 and 8 cm, preferably between 4 and 6 cm. Thegranular solid or granulate can preferably be composed of a multiplicityof substantially spherical particles. The sorption material ZEO embodiedas a granular solid or granulate advantageously usefully has an averagefill density of at least 500 kg/m³, in particular substantially between500 and 800 kg/m³, in particular between 600 and 700 kg/m³, inparticular between 630 and 650 kg/m³, in particular preferably ofapproximately 640 kg/m³.

In the sorption container SB, the reversibly dehydratable sorptionmaterial ZEO for absorbing a quantity of moisture transported in the airflow LS2 is usefully provided in a quantity by weight such that thequantity of moisture absorbed by the sorption material ZEO is lower thana quantity of moisture applied to the items to be washed, in particulara quantity of moisture applied in the rinsing step.

It can in particular be useful if in the sorption container SB thereversibly dehydratable sorption material is provided in a quantity byweight such that this is sufficient to absorb a quantity of moisturewhich corresponds substantially to a wetting quantity with which theitems to be washed are wetted after the end of a rinsing step. Theabsorbed quantity of water corresponds preferably to between 4 and 25%,in particular between 5 and 15%, of the quantity of liquid applied tothe items to be washed.

The sorption container usefully accommodates an amount by weight ofsorption material ZEO of substantially between 0.2 and 5 kg, inparticular between 0.3 and 3 kg, preferably between 0.5 and 2.5 kg.

The sorption material ZEO has in particular pores preferably ofsubstantially between 1 and 12 Angstroms, in particular between 2 and10, preferably between 3 and 8 Angstroms, in size.

It usefully has a water absorption capacity of substantially between 15and 40 percent, preferably between 20 and 30 percent of its dry weight.

In particular, a sorption material is provided which can be desorbed ata temperature substantially in the range between 80° and 450° C., inparticular between 220° C. and 250° C.

The air-guiding channel, the sorption container, and/or one or moreadditional flow-influencing elements are usefully embodied such that anair flow can be effected through the sorption material for the sorptionand/or desorption thereof with a volume flow of substantially between 2and 15 l/sec, in particular between 4 and 7 l/sec.

It can in particular be useful if at least one heating device HZ isassigned to the sorption material ZEO, by means of which heating devicean equivalent heat output of between 250 and 2500 W, in particularbetween 1000 and 1800 W, preferably between 1200 and 1500 W can beprovided for heating the sorption material for the desorption thereof.

The ratio of heat output of at least one heating device which isassigned to the sorption material for the desorption thereof and airvolume flow of the air flow which flows through the sorption material ispreferably chosen so as to be between 100 and 1250 W sec/l, inparticular between 100 and 450 W sec/l, preferably between 200 and 230 Wsec/l.

In the sorption container, a through-flow cross-sectional area for thesorption material of substantially between 80 and 800 cm², in particularbetween 150 and 500 cm², is preferably provided.

The fill height H of the sorption material ZEO via the inletcross-sectional area SDF of the sorption container SB is usefullysubstantially constant.

It is in particular useful to embody the sorption material in thesorption container SB so as to absorb a quantity of water ofsubstantially between 150 and 400 ml, in particular between 200 and 300ml.

Furthermore, for at least one component of the sorption drying systemTS, at least one thermal overheating-protection device TSI (see FIGS. 4,6, 8, 9) is provided. Such a component can preferably be formed by acomponent of the sorption container SB. At least one thermaloverheating-protection device TSI can be assigned to this component.This thermal overheating-protection device TSI is affixed to the outsideof the sorption container SB. At least one electrical temperatureprotection unit is provided as a thermal overheating-protection device.It is assigned in the exemplary embodiment here to the heating device HZwhich is accommodated in the sorption container SB.

The electrical temperature-protection unit is provided in the exemplaryembodiment of FIGS. 4, 6, 8 and 9 in an outside recess EBU on the innerhousing IG of the sorption container SB in the region of the verticalposition of the heating device HZ. It comprises at least one electricalthermal switch TSA and/or at least one fuse SSI (see FIG. 17). Theelectrical thermal switch TSA and/or the fuse SSI of the electricaltemperature-protection unit TSI are respectively inserted, preferably inseries, into at least one electrical power supply line UB1, UB2 of theheating device HZ (see FIG. 8).

It can furthermore be useful to provide at least one control device HE,ZE (see FIG. 16) which in particular in the case of a fault interruptsthe power supply to the heating device HZ. The exceeding of an uppertemperature limit, for example, constitutes a fault case.

Furthermore, the largely freely-hanging suspension of the sorptioncontainer, particularly underneath the base BO of the washing containerSPB, can also serve as a thermal overheating-protection device.

The thermal overheating-protection device can furthermore comprise apositioning of the sorption container SB such that the sorptioncontainer has a predefined minimal gap distance LSP in relation toneighboring components and/or parts of a base module BG.

As a thermal overheating-protection device, there can be provided inaddition to, or independently of, the measures indicated above, at leastin the region of the sorption unit SE of the sorption container SB atleast one outer housing AG in addition to the inner housing IG of thesorption container SB. Between the inner housing IG and the outerhousing AG, an air gap clearance LS is present as a thermal insulationlayer.

The coiled-tube heater HZ of FIGS. 4, 7, 8, 9 comprises two terminalpoles AP1, AP2 which are guided outwardly through correspondingthrough-openings in the housing of the washing container SPB. Eachterminal pole or terminal pin AP1, AP2 is preferably switched in serieswith an overheating-protection element. The overheating-protectionelements are grouped in the temperature protection unit TSI which isarranged externally on the housing of the sorption container SB in thevicinity of the two pole pins AP1, AP2. FIG. 17 shows theoverheating-protection circuit for the coiled-tube heater HZ from FIG.8. The first bypass line UB1 is attached to the first rigid pole pin AP1by means of a welded connection SWE1. In an analogous manner, the secondbypass line UB2 is attached to the second rigid pole pin AP2 by means ofa welded connection SWE2. By means of a plug-in connection SV4, thebypass line UB2 is electrically contacted to the thermal switch TSA. Thebypass line UB1 is electrically connected via a plug-in contact SV3 tothe thermoelectric fuse SSI. At the input end, a first power supply lineSZL1 is connected via a plug-in connection SV1 to the outwardly guidedterminal lug AF1 of the fuse element SSI. In an analogous manner, asecond power supply line SZL2 is connected via a plug-in connection SV2to the outwardly guided terminal lug AF2 of the thermal switch elementTSA. The second power supply line SZL2 can, in particular, form aneutral conductor, while the first power supply line SZL1 can be a “livephase”. The thermal switch TSA opens as soon as a first upper limit forthe temperature of the coiled-tube heater HZ is exceeded. As soon as thetemperature falls below this limit again, it closes again so that thecoiled-tube heater HZ is heated up once again. If, however, a criticalupper temperature limit, which lies above the first upper limit, for thecoiled-tube heater HZ is reached, then the fuse SSI melts through andthe electric circuit for the coiled-tube heater HZ is permanentlyinterrupted. The two temperature-protection elements of thetemperature-protection device TSI are in largely intimateheat-conducting contact with the inner housing IG of the sorptioncontainer. They can be separately detached from one another if certainupper temperature limits specifically assigned to them are exceeded.

In accordance with FIGS. 10, 13, 14, the outflow connecting piece AKTwhich is connected to the outlet opening AO in the socket SO of thesorption container SB passes through the through-opening GK in the baseBO preferably in a corner region EBR of the washing container SPB whichlies outside the area of rotation swept over by the spray arm SA. Thisis illustrated in FIG. 2. Expressed in general terms, the outflowconnecting piece AKT thus projects out of the base BO into the interiorof the washing container SPB at a point which lies outside the area ofrotation covered by the lower spray arm SA. The exhaust chimneyconnecting piece or the outflow connecting piece AKT is overlapped orcovered over along its upper end portion by a spray-protection hood SH.

The spray-protection hood SH covers over the outflow connecting pieceAKT in an umbrella-like or mushroom-like manner. This spray-protectionhood is, viewed from above (see FIG. 12) completely closed on thetop-side; it is also, in particular, also completely closed on itsunderside in a region facing the spray arm SA. It exhibits in theexemplary embodiment here in a first approximation the geometric shapeof a semi-circular cylinder. The spray-protection hood SH is representedschematically, viewed from above, in FIG. 12. On its top side, it has inthe transition zones GF, URA between its largely planar top side and itssubstantially vertically downwardly projecting side walls (viewed frominside to outside) convexly curved flattening portions GF (see FIG. 13).If a spray jet, e.g. from the spray arm SA, strikes these transitionzones GF, URA which are flattened out on the top edge or curved, thenthis spray jet pours like a film largely over the full surface of thespray-protection hood SH and cools this hood during the desorptionprocess.

In order to prevent liquid during spraying with the lower spray arm SAfrom being able to pass through the discharge opening of the outflowconnecting piece AKT into the sorption container SB, a lower edge zoneUR of the semi-circular-cylinder-portion-like side wall of the sprayprotection hood SH is curved, arched or bent inwardly toward the outflowconnecting piece AKT. This can readily be seen in FIG. 13. In addition,in the region of the top edge of the outflow connecting piece AKT, anencircling and radially outwardly projecting spray-water deflectingelement or shielding element PB, in particular a baffle plate, isprovided. This shielding element projects radially outwardly into theintermediate space or gap space between the cylindrical outflowconnecting piece AKT and the inner wall of the spray-protection hood SH.Between the outer peripheral edge of this shielding element PB and theinner wall of the spray-protection hood SH there remains a freethrough-opening for the air flow which flows out from the outflowconnecting piece AKT in the direction of the cover of thespray-protection hood SH and in doing so is diverted downwardly to thelower edge UR of the spray-protection hood SH, in particular byapproximately 180°. The deflection path is labeled ALS in FIG. 13. Theoutwardly projecting shielding element PB is supported in the exemplaryembodiment of FIG. 13 at individual circumferential points of its outeredge by means of web elements SET against the inner wall of the sidewall of the spray-protection hood SH which encircles in the form of aring segment portion. The spray-protection hood SH is arranged at a freevertical distance opposite the outlet connecting piece AKT, forming afree space or cavity.

FIG. 14 shows the spray-protection hood SH, viewed from below, togetherwith the outflow connecting piece AKT. The shielding element PB shieldsthe discharge opening of the outflow connecting piece AKT as a laterallyor sideways projecting edge or web in a substantially circumferentialmanner. In particular, the shielding element PB closes off the undersideof the spray-protection hood SH in the region of the rectilinear sidewall facing the spray arm SA. Only in the semi-circularly bent portionof the spray-protection hood SH facing away from the spray arm betweenthe shielding element PB and the externally concentrically arranged sidewall of the spray-protection hood SH running in a radially offset manneris a gap clearance LAO cleared through which the air can flow out fromthe outflow connecting piece AKT into the interior of the washingcontainer SPB. In the exemplary embodiment here from FIG. 14, the gapclearance LAO is substantially embodied in a sickle-like manner. The airflow LS2 is forced thereby onto the diverted path ALS which diverts itfrom its vertically upwardly oriented outflow direction downward whereit can exit only through the sickle-shaped gap clearance LAO in theshape of a segment of a divided circle in the lower region of thespray-protection hood SH. The outflow connecting piece AKT usefullyprojects to a height HO relative to the base BO such that its top edgelies higher than the level of a set total wash-tank volume or foamvolume envisaged for a wash cycle.

The outflow element AUS which is affixed at the outlet end of thesorption container SB and projects into the interior of the washingcontainer SPB is therefore usefully embodied such that the air flow LS2exiting from it is directed away from the spray arm SA. In particular,the outflowing air flow LS2 is guided into a rear or back corner regionbetween the back wall RW and the adjacent side wall SW of the washingcontainer. This largely prevents spray-water or foam from being able topass through the opening of the outflow connecting piece into theinterior of the sorption container during the cleaning cycle or anyother wash cycle. The desorption process could otherwise be impaired orcompletely nullified in this way. In addition, sorption material couldbe permanently damaged by washing solution. Extensive tests have in factshown that the functionality of the sorption material in the sorptioncontainer can be largely retained or preserved over the life time of thedishwasher if water, detergent and/or rinse aid in the washing solutionis reliably prevented from reaching the sorption material.

In summary, at least one outflow device AUS which is connected to atleast one outflow opening AO of the sorption container SB is arranged inthe interior of the washing container SPB such that air LS2 blown outfrom it is largely directed away from at least one spray device SAaccommodated in the washing container SPB. The outflow device AUS isarranged outside the working area of the spray device SA. The spraydevice can be e.g. a rotating spray arm SA. The outflow device AUS ispreferably provided in a rear corner region EBR between the back wall RWand an adjacent side wall SW of the washing container SPB. The outflowdevice AUS has in particular an exhaust opening ABO at a verticaldistance HO above the base BO of the washing container SPB, said exhaustopening lying higher than the level of a set total wash-tank volumeenvisaged for a wash cycle. The outflow device AUS comprises an outflowconnecting piece AKT and a spray-protection hood SH. Thespray-protection hood SH has a geometric shape which slips over theexhaust opening ABO of the outflow connecting piece AKT. Thespray-protection hood SH is slipped over the outflow connecting pieceAKT such that air flowing up through the outflow connecting piece AKTout of the sorption container SB with a rising direction of flow can,after its exit from the exhaust opening ABO of the outflow connectingpiece AKT, have a downwardly directing forced flow path ALS impressedupon it. The upwardly projecting outflow connecting piece AKT above thebase BO of the washing container SPB is coupled to the terminalconnecting piece STE on the cover part DEL of the sorption container SBarranged under the base BO. The spray-protection hood SH is, in itshousing region GF facing the spray device SA, embodied in a closedmanner both on the top and on the underside. The spray-protection hoodSH overlaps the exhaust opening ABO of the outflow connecting piece AKTwith an upper free space. The outflow connecting piece AKT has an upper,outwardly arched edge or circumferential collar KR. The spray-protectionhood SH envelops an upper end portion of the outflow connecting pieceAKT so as to form a gap clearance SPF between its inner wall and theouter wall of the outflow connecting piece AKT. The gap clearance SPFbetween the spray-protection hood SH and the outflow connecting pieceAKT is embodied such that an air outflow path ALS out of the outflowconnecting piece AKT is provided which is directed away from the spraydevice SA in the washing container SB. A spray-water deflecting elementPB projecting into the gap clearance SPF is provided on theoutflow-connecting piece AKT. A lower edge zone UR of thespray-protection hood SH is arched inwardly. The spray-protection hoodSH has a rounded outer surface such that it causes a spray jet from thespray device SA which strikes it to pour over its surface like a film.

FIG. 15 shows a schematic longitudinal representation of the fixing ofthe inlet-side, frontal end portion ET of the air-guiding channel LK inthe region of the outlet opening ALA in the side wall SW of the washingcontainer SPB of FIG. 2. The frontal end portion ET of the air-guidingchannel LK projects into the interior of the washing container SPB suchthat a collar edge is formed circumferentially projectingperpendicularly in relation to the side wall SW. This collar edge has aninternal thread SG. An annular inlet element IM with an external threadis screwed into this internal thread SG. It therefore functions as afixing element for holding the end portion ET. This annular fixingelement has a toroidal encircling receiving chamber for a sealingelement DI2. This sealing element DI2 seals an annular gap between theouter edge of the inlet-side frontal end portion ET of the air-guidingchannel LK and the fixing element. The fixing element in the exemplaryembodiment here is formed in particular by a screw-cap-like threadedring which is screwed to the inlet-side frontal end portion ET of theair-guiding channel LK. In the exemplary embodiment, the annular fixingelement IM has a central through passage MD through which air LU can besucked out of the interior of the washing container SPB.

It can optionally also be useful to provide in or in front of the inletopening MD of the inlet-end tube portion ET of the air-guiding channelLK at least one ribbed engagement protection which has between itsengagement ribs RIP freely passable gaps for the inflow of air out ofthe washing container. These ribs RIP are indicated in FIG. 15 by dashedand dotted lines.

FIG. 16 shows in schematic plan view representation the base module BG.It comprises in addition to the fan unit LT, the sorption container SB,the circulating pump UWP, etc. . . . a main control device HE for thecontrol and monitoring thereof. The heating device HZ of the sorptioncontainer SB is also regulated for the desorption process thereof bymeans of at least one control device. This control device is formed inthe exemplary embodiment here by an additional control device ZE. Itserves to interrupt or switch through the power supply line SZL to theheating device HZ as required. The additional control device ZE iscontrolled from the main control device HE via a bus line BUL. A powersupply line SVL runs from the main control device HE to the additionalcontrol device ZE. This additional control device also controls via acontrol line SLL the fan unit LT. The power supply line to the fan unitLT can in particular also be integrated into the control line SLL.

Also connected to the main control device HE via a signal line is atleast one temperature sensor TDE (see FIG. 2) which deliverscorresponding measurement signals for the temperature in the interior ofthe washing container to the main control device. The temperature sensorTSE is suspended between stiffening ribs VR (see FIG. 3) in theintermediate space between the two arms of the inlet-end tube portionRA1 of the air-guiding channel LK. It is thereby brought into contactwith the side wall SW of the washing container SPB.

As soon as a cleaning cycle is now started, the main control device HEsimultaneously switches on the additional control device ZE via the busline BUL such that an electrical voltage is applied via the power supplyline SZL to the pole pins AP1, AP2 of the heating device HZ if adesorption process is desired. As soon as a certain predeterminedcritical upper temperature limit has been reached during the desorptionprocess in the interior of the washing container SPB, which the maincontrol device HE can determine e.g. via the measurement signals of thetemperature sensor, it can give the instruction to the additionalcontrol device ZE via the bus line BUL to withdraw the voltage on thepower supply line SZL and thereby to switch off the heating device HZcompletely. In this way, e.g. the desorption process for the sorptionmaterial in the sorption container can be terminated.

It can optionally be useful to provide for a person operating thedishwasher the option of activating or deactivating the sorption dryingsystem TS through activation or deactivation of a specially providedprogram button or through corresponding selection of a program menu.This is illustrated schematically in FIG. 16 in that included in thedrawing is a program button or a program menu item PG1 which givesappropriate activation or deactivation signals for switching on andswitching off the sorption drying system TE via a control line SL1 bymeans of control signals SS1 to the control logic HE.

In particular, a first selection button for selecting an “Energy” or“Sorption operation” program variant can be provided in the controlpanel. In this program, the emphasis is on saving energy. This isachieved in that during the rinse cycle no heating at all is carried outby means of a continuous-flow heater and the drying of the washed items,in particular of the crockery, is effected solely with the aid of thesorption drying system TS.

It can be useful in particular, in addition to pure sorption drying, toheat the interior of the washing container during the rinse cyclethrough heated final rinse liquid. It can advantageously be sufficientif the transfer of heat to the items to be dried which is effected bymeans of the final rinse cycle is achieved with lower use of energy thanis the case with no sorption drying. For electrical heat energy can,through sorption of air humidity, be saved by means of the sorptiondrying system now used. Thus, improved drying of wet and moist items tobe washed can be achieved both by means of so-called “intrinsic-heatdrying” and also by means of sorption drying, i.e. through a combinationor addition of the two drying types.

In addition to or independently of the “Energy” button, a further“Drying performance” button can be provided in the control panel of thedishwasher which increases the blower run time of the fan unit. Improveddrying of all crockery items can be achieved by this means.

In addition to or independently of the above special buttons, a further“Program run time” button can be provided. If the sorption drying systemis switched on, the program run time can be reduced compared withconventional drying systems (without sorption drying). The run timeduring cleaning can optionally be further shortened through additionalheating in the cleaning phase and optionally by increasing the spraypressure by increasing the motor speed of the circulating pump.Furthermore, the drying time can also be further shortened by increasingthe rinse temperature.

In addition to or independently of the previous specific buttons, anactuation button with the function “Influence the cleaning performance”button can be provided. By actuating this button, the cleaningperformance can be enhanced over the same run time without energyconsumption being increased compared to a dishwasher without a sorptiondrying system. For heat energy for heating a desired total quantity ofliquid in the wash tank can be saved in that, during a prewash and/orcleaning cycle, the desorption process is started at the same time andhot air, laden with a quantity of water discharged by the sorptionmaterial, passes into the washing container as a result.

1-33. (canceled)
 34. A dishwasher, comprising: a washing container; anair-guiding channel to generate air flow; and a sorption drying systemto dry items to be washed, wherein the sorption drying system has asorption container with reversibly dehydratable sorption material, thesorption container connected to the washing container by the air-guidingchannel; wherein the reversibly dehydratable sorption material in thesorption container is one of a granular solid and a granulate having aplurality of particles as a fill with a grain size substantially between1 mm and 6 mm; and wherein a fill height of the plurality of particlesis at least 5 times the grain size of the plurality of particles. 35.The dishwasher of claim 34, wherein the dishwasher is a householddishwasher, and wherein the grain size is between 2.4 mm and 4.8 mm. 36.The dishwasher of claim 34, wherein the reversibly dehydratable sorptionmaterial contains at least one of aluminum and silicon-oxide, andwherein the reversibly dehydratable sorption material is at least one ofsilica gel and zeolite.
 37. The dishwasher of claim 36, wherein thezeolite is of at least one of type A, X, and Y.
 38. The dishwasher ofclaim 34, wherein, in a direction of gravity, the reversiblydehydratable sorption material in the sorption container is one of agranular solid and a granulate with a fill height of substantially 5times to 40 times a particle size of the one of the granular solid andthe granulate.
 39. The dishwasher of claim 38, wherein the fill heightof the reversibly dehydratable sorption material is substantially 10times to 15 times the particle size.
 40. The dishwasher of claim 38,wherein the fill height of the reversibly dehydratable sorption materialis substantially between 1.5 cm and 25 cm.
 41. The dishwasher of claim40, wherein the fill height of the reversibly dehydratable sorptionmaterial is between 2 cm and 8 cm.
 42. The dishwasher of claim 41,wherein the fill height of the reversibly dehydratable sorption materialis between 4 cm and 6 cm.
 43. The dishwasher as of claim 38, wherein theone of the granular solid and the granulate has a plurality ofsubstantially spherical particles.
 44. The dishwasher of claim 34,wherein the reversibly dehydratable sorption material is embodied as oneof a granular solid or granulate with an average fill density of atleast 500 kg/m³.
 45. The dishwasher of claim 44, wherein the averagefill density of the reversibly dehydratable sorption material issubstantially between 500 kg/m³ and 800 kg/m³.
 46. The dishwasher ofclaim 45, wherein the average fill density of the reversiblydehydratable sorption material is substantially between 600 kg/m³ and700 kg/m³.
 47. The dishwasher of claim 46, wherein the average filldensity of the reversibly dehydratable sorption material issubstantially between 630 kg/m³ and 650 kg/m³.
 48. The dishwasher ofclaim 47, wherein the average fill density of the reversiblydehydratable sorption material is approximately 640 kg/m³.
 49. Thedishwasher of claim 34, wherein, in the sorption container, thereversibly dehydratable sorption material absorbs a first moisturequantity transported in the air flow in a quantity by weight such thatthe first moisture quantity absorbed by the reversibly dehydratablesorption material is lower than a second moisture quantity applied tothe items to be washed.
 50. The dishwasher of claim 49, wherein thesecond moisture quantity is applied in a rinsing step.
 51. Thedishwasher of claim 34, wherein, in the sorption container, thereversibly dehydratable sorption material has a quantity by weightsufficient to absorb a moisture quantity which corresponds substantiallyto a wetting quantity with which the items to be washed are wetted afterthe end of a final rinsing step.
 52. The dishwasher of claim 34, whereina water quantity absorbed by the reversibly dehydratable sorptionmaterial corresponds to between 4% and 25% of a liquid quantity appliedto the items to be washed.
 53. The dishwasher of claim 52, wherein thewater quantity corresponds to between 5% and 15% of the liquid quantity.54. The dishwasher of claim 34, wherein the reversibly dehydratablesorption material accommodated in the sorption container has an amountby weight of substantially between 0.2 kg and 5 kg.
 55. The dishwasherof claim 54, wherein the amount by weight of the reversibly dehydratablesorption material is substantially between 0.3 kg and 3 kg.
 56. Thedishwasher of claim 55, wherein the amount by weight of the reversiblydehydratable sorption material is substantially between 0.5 kg and 2.5kg.
 57. The dishwasher of claim 34, wherein the reversibly dehydratablesorption material in the sorption container absorbs a water amount ofsubstantially between 150 ml and 400 ml.
 58. The dishwasher of claim 57,wherein the water amount is substantially between 200 ml and 300 ml. 59.The dishwasher of claim 34, wherein the reversibly dehydratable sorptionmaterial has pores of substantially between 1 Angstroms and 12 Angstromsin size.
 60. The dishwasher of claim 59, wherein the reversiblydehydratable sorption material has pores of substantially between 2Angstroms and 10 Angstroms size.
 61. The dishwasher of claim 60, whereinthe reversibly dehydratable sorption material has pores of substantiallybetween 3 Angstroms and 8 Angstroms in size.
 62. The dishwasher of claim34, wherein the reversibly dehydratable sorption material has a waterabsorption capacity of substantially between 15% and 40% of a dry weightof the reversibly dehydratable sorption material.
 63. The dishwasher ofclaim 62, wherein the water absorption capacity is substantially between20% and 30% of the dry weight of the reversibly dehydratable sorptionmaterial.
 64. The dishwasher of claim 34, wherein the reversiblydehydratable sorption material is desorbed at a temperaturesubstantially in the range between 80° C. and 450° C.
 65. The dishwasherof claim 64, wherein the range is between 220° C. and 250° C.
 66. Thedishwasher of claim 34, further comprising an additionalflow-influencing element, wherein at least one of the air-guidingchannel, the sorption container, and the additional flow-influencingelement is embodied such that the air flow is effected through thereversibly dehydratable sorption material with a volume flow ofsubstantially between 2 l/sec and 15 l/sec for at least one of sorptionand desorption of the reversibly dehydratable sorption material.
 67. Thedishwasher of claim 66, wherein the volume flow is between 4 l/sec and 7l/sec.
 68. The dishwasher of claim 34, further comprising a heaterassigned to the sorption material, the heater generating an equivalentheat output of between 250 W and 2500 W to heat the reversiblydehydratable sorption material for desorption of the reversiblydehydratable sorption material.
 69. The dishwasher of claim 68, whereinthe equivalent heat output is between 1000 W and 1800 W.
 70. Thedishwasher of claim 69, wherein the equivalent heat output is between1200 W and 1500 W.
 71. The dishwasher of claim 34, further comprising aheater assigned to the reversibly dehydratable sorption material fordesorption of the reversibly dehydratable sorption material, wherein aratio of a heat output of the heater and an air volume flow of the airflow which flows through the reversibly dehydratable sorption materialis between 100 W sec/l and 1250 W sec/l.
 72. The dishwasher of claim 71,wherein the ratio is between 100 W sec/l and 450 W sec/l.
 73. Thedishwasher of claim 72, wherein the ratio is between 200 W sec/l and 230W sec/l.
 74. The dishwasher of claim 34, wherein, in the sorptioncontainer, a through-flow cross-sectional area for the reversiblydehydratable sorption material of substantially between 80 cm² and 800cm² is provided.
 75. The dishwasher of claim 74, wherein thethrough-flow cross-sectional area is between 150 cm² and 500 cm². 76.The dishwasher of claim 34, wherein the sorption container has asorption unit, and wherein a fill height of the reversibly dehydratablesorption material is substantially constant across an inletcross-sectional area of the sorption unit.
 77. The dishwasher of claim34, further comprising a base module, wherein the washing container hasa base, wherein the base module is arranged underneath the base of thewashing container, and wherein the sorption container is arranged in thebase module.
 78. The dishwasher of claim 34, wherein the air-guidingchannel is arranged substantially outside the washing container.
 79. Thedishwasher of claim 34, further comprising a fan; wherein theair-guiding channel has an inlet-side tube portion; wherein the sorptioncontainer has an entry opening; and wherein, when viewed in a flowdirection, the fan is inserted upstream of the sorption container intothe inlet-side tube portion of the air-guiding channel to generate aforced air flow in the direction towards the entry opening of thesorption container.
 80. The dishwasher of claim 79, further comprising abase module underneath the washing container, wherein the fan isarranged in the base module.
 81. The dishwasher of claim 34, wherein thesorption container has a base, wherein the air-guiding channel iscoupled to the sorption container such that the air flow flows into anarea of the sorption container close to the base with an inflowdirection and changes into a through-flow direction, which is differentfrom the inflow direction and with which the air flow flows through theinterior of the sorption container.
 82. The dishwasher of claim 81,wherein the inlet-side tube portion of the air-guiding channel opens outinto the sorption container such that an inflow direction of theinlet-side tube portion is diverted into the through-flow direction ofthe sorption container.
 83. The dishwasher of claim 82, wherein theinflow direction is diverted by approximately 90°.
 84. The dishwasher ofclaim 34, wherein the sorption container has an inlet opening; whereinthe reversibly dehydratable sorption material in the interior of thesorption container has a through-flow cross-sectional area; wherein theair-guiding channel has an inlet connecting piece with a passagecross-sectional area with which the air-guiding channel opens into theinlet opening of the sorption container; and wherein the through-flowcross-sectional area for the reversibly dehydratable sorption materialis greater than the passage cross-sectional area of the inlet connectingpiece of the air-guiding channel.
 85. The dishwasher of claim 84,wherein the through-flow cross-sectional area of the sorption containeris between 2 times and 40 times greater than the passage cross-sectionalarea of the inlet connecting piece on an end of the air-guiding channelwith which the air-guiding channel opens into the inlet opening of thesorption container.
 86. The dishwasher of claim 85, wherein thethrough-flow cross-sectional area of the sorption container is between 4times and 30 times greater than the passage cross-sectional area of theinlet connecting piece on the end of the air-guiding channel with whichthe air-guiding channel opens into the inlet opening of the sorptioncontainer.
 87. The dishwasher of claim 86, wherein the through-flowcross-sectional area of the sorption container is between 5 times and 25times greater than the passage cross-sectional area of the inletconnecting piece on the end of the air-guiding channel with which theair-guiding channel opens into the inlet opening of the sorptioncontainer.
 88. The dishwasher of claim 34, wherein the sorptioncontainer accommodates a sorption unit having the reversiblydehydratable sorption material such that air flows through thereversibly dehydratable sorption material substantially in or againstthe direction of gravity, and wherein the air is guided out of thewashing container into the sorption container via the air-guidingchannel.
 89. The dishwasher of claim 88, wherein the sorption unit hasone of a lower sieve element and a lower grid element and one of anupper sieve element and an upper grid element at a predefined verticaldistance from one another, and wherein a spatial volume between the oneof the two sieve elements and the two grid elements is substantiallycompletely filled with the reversibly dehydratable sorption material.90. The dishwasher of claim 34, further comprising a heater, wherein,when viewed against the direction of gravity, the sorption container hasa layer having the heater, an intermediate space downstream from theheater, and a subsequent sorption unit.
 91. The dishwasher of claim 90,wherein, when viewed in a through-flow direction of the sorptioncontainer, the heater is arranged upstream of the sorption unit of thesorption container.
 92. The dishwasher of claim 34, wherein the sorptioncontainer has a base, and wherein the heater is arranged in a lowercavity close to the base of the sorption container.
 93. The dishwasherof claim 34, wherein the air-guiding channel has an inlet-end tubeportion, and wherein a flow-conditioning element is arranged in at leastone of the sorption container and the inlet-end tube portion of theair-guiding channel such that equalization of a local flowcross-sectional profile of the air flow is effected when flowing throughthe sorption container in a through-flow direction of the sorptioncontainer.